US3472038A - Apparatus and method for transferring heat from a lower temperature level to a higher temperature level - Google Patents

Apparatus and method for transferring heat from a lower temperature level to a higher temperature level Download PDF

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US3472038A
US3472038A US722693A US3472038DA US3472038A US 3472038 A US3472038 A US 3472038A US 722693 A US722693 A US 722693A US 3472038D A US3472038D A US 3472038DA US 3472038 A US3472038 A US 3472038A
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duct
superfluid
helium
superleak
temperature
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US722693A
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Frans Adrianus Staas
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US Philips Corp
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US Philips Corp
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/12Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using 3He-4He dilution

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  • An apparatus and method for transferring heat from low to high temperature levels includes a pump to flow only superfluid He through a superleak, whereby its temperature is reduced, to a thermally insulated container where a portion of this He absorbs heat from an object to be cooled and is converted to normal He", and remaining superfluid He flows turbulently through a return duct, entraining with it the heat-carrying normal He*.
  • the invention relates to an apparatus and method for transferring heat from a lower to a higher temperature level, which is characterized in that both temperature levels lie below the temperature of the point of helium.
  • the apparatus includes a circulating duct which is filled with He and accommodates at least one body of material which is characterized in that normal He cannot pass through it, but superfluid He can, without giving rise to moving turbulence (superleak); this material extends along part of the duct and completely occupies its internal cross-sectional area.
  • the circulating duct includes a pumping device capable of maintaining a pressure difference across this body.
  • the said body and at least part of the duct situated at the lower-pressure side of the body are thermally insulated, and the part of the duct in communication with the higher-pressure side of the body being in thermal contact with a cooler in which a temperature prevails below the point of He.
  • the dimensions of the internal cross-sectional area of the duct and the pumping device are chosen so that in flowing through them, the medium exceeds its critical velocity with consequent turbulence.
  • the body of material characterized in that normal He cannot flow through it, but superfluid He* can without the occurrence of turbulence, will hereinafter be referred to as a superleak.
  • the apparatus in accordance with the invention utilizes the fact that when in a U-shaped tube containing He at a temperature below the point, there is provided a superleak across which a temperature difference prevails, a driving force is exerted on the superfluid helium which causes it to flow through the superleak towards the high temperature.
  • This flow of superfluid helium continues until there is produced in the limbs of the U-shaped tube a difference in level which produces a pressure difference across the superleak, which compensates for the driving force which acts on the superfluid helium owing to the temperature diiference.
  • the production of a pressure difference across the superleak will give rise to a temperature diiference across it.
  • the apparatus according to the invention is based on the recognition that a continuous cooling process is obtained owing to the fact that turbulence will occur in the superfluid helium in the circulating duct, and that owing to the interaction of the turbulence in the superfluid helium on the normal helium, the latter will be carried along by the flow of superfluid helium.
  • This entrained normal helium exhibits entropy and hence heat will be carried along by this normal helium from the cold area to the cooled area at the higher temperature.
  • This provides a surprisingly simple apparatus by means of which, starting from a temperature below the A point of the helium, cold may be produced at lower temperatures.
  • the thermally insulated part of the device is disposed in a vacuum chamber which is surrounded by a bath of liquid He at a temperature below the A point, the part of the duct protruding from the vacuum chamber being also surrounded by the liquid He.
  • the pumping device takes the form of a centrifugal pump disposed in the part of the duct protruding from the thermal insulation.
  • the circulating duct need not be a closed duct of constant cross-section.
  • the nonthermally insulated part i.e. the part at the higher temperature, may include a container which is also filled with He*.
  • the part of the duct situated in the path of the liquid He may be interrupted.
  • the He bath ellectively forms part of the duct. This is possible since the duct contains the same medium as the surrounding bath.
  • FIG- URES 1 and 2 show schematically and not to scale two embodiments of the apparatus in accordance with the invention.
  • the apparatus shown in FIGURE 1 includes a circulating duct 1, containing He A pumping device 2, a superleak 3 and a container 4 are disposed in the duct.
  • the part of the duct constituted by the superleak 3, the container 4- and a pipe 5, is located in a vacuum chamber 6 which, through a pipe 7, is connected to a vacuum pump, not shown, to maintain the desired vacuum in the chamher 6.
  • the part of the duct 1 protruding from the chamber 6 and accommodating the pump 2 is surrounded by liquid He which also surrounds the chamber 6 and is contained in a Dewar flask.
  • the vapour pressure above the liquid helium in the Dewar flask 8 is reduced to a value such that the temperature of the liquid helium in the flask 8 is lower than the temperature of the A point of helium.
  • the temperature may, for example, be 13 K.
  • the pump 2 is connected through a shaft 9 to a driving device, not shown.
  • the apparatus operates as follows: On rotation of the pump 2 a higher pressure will be produced on the upper side of the superleak 3 at the area 10 and will drive the superfluid helium through the superleak.
  • the superleak 3 may be in the form of pressed or sintered very finely divided substances, such as carborundum or iron oxide.
  • the part 5 of the duct is proportioned so that the superfluid helium exceeds its critical velocity therein with consequent turbulence. Owing to the interaction of the turbu- 3 lence of the superfluid helium, part of the normal helium will be carried along towards the pump. By this normal helium, heat will be carried away from the container 4 towards the pump. At an area 12 the circulating medium comes into heat-exchange with the helium bath so that it will again be brought to the temperature of this bath. Thus, an amount of heat will be transferred from the container 4, which is at a low temperature of, for example, 0.7 K., to the helium bath, which is at a temperature of, say, 1.3 K.
  • This provides a cooling apparatus in which the superfluid helium when flowing through the superleak 3 to the container 4 transfers no heat, whereas the superfluid helium when flowing from the container 4 to the pump 2 through the capillary 5, in which turbulence occurs, is capable of entraining some normal helium so as to produce heat convection.
  • FIGURE 2 shows an apparatus which broadly corresponds to the apparatus shown in FIGURE 1. The difference is that the part of the duct 1 which is surrounded by the He bath is interrupted so that the capillary opens into the bath and the suction side of the pump 2 is connected to the bath. Thus, the bath efiFectively forms a buffer chamber for the duct. The operation of this apparatus is identical to that of the apparatus of FIGURE 1.
  • a method as defined in claim 1 comprising the further steps of pumping said superfluid He through said superleak.
  • a method as defined in claim 2 comprising the further steps of flowing said superfluid He and normal He from said container to a pump, pumping said He to said superleak, and cooling said He to a temperature below the A point before it reaches the superleak.
  • a method as defined in claim 3 comprising the further steps of immersing said pump, container and duct in a quantity of superfluid He within a Dewar.
  • (c) means for cooling the fiuid entering the high-pressure side of the superleak to a temperature below the A point of He;
  • the duct being dimensioned such that superfluid He is fiowable therethrough from the container at a greater than critical velocity and to thereby flow turbulently and entrain the normal He into which heat from said object is absorbable.
  • Apparatus as defined in claim 5 wherein said means for providing a pressure difference is a pump.
  • Apparatus as defined in claim 5 further comprising a vacuum chamber housing for providing said thermal insulation.
  • Apparatus as defined in claim 7 further comprising a Dewar containing liquid He at a temperature below its )1 point and in which said chamber and means for providing a pressure difference are immersed.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Containers, Films, And Cooling For Superconductive Devices (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)

Description

Oct. 14, 1969 F. A. STAAS 3,472,038
APPARATUS AND METHOD FOR TRANSFERRING REAT FROM A LOWER TEMPERATURE LEVEL TO A HIGHER TEMPERATURE LEVEL Filed April 19, 1968 INVENTOR. FRANS A.STAAS AGENT United States Patent US. CI. 62-45 Claims ABSTRACT OF THE DISCLOSURE An apparatus and method for transferring heat from low to high temperature levels includes a pump to flow only superfluid He through a superleak, whereby its temperature is reduced, to a thermally insulated container where a portion of this He absorbs heat from an object to be cooled and is converted to normal He", and remaining superfluid He flows turbulently through a return duct, entraining with it the heat-carrying normal He*.
The invention relates to an apparatus and method for transferring heat from a lower to a higher temperature level, which is characterized in that both temperature levels lie below the temperature of the point of helium. The apparatus includes a circulating duct which is filled with He and accommodates at least one body of material which is characterized in that normal He cannot pass through it, but superfluid He can, without giving rise to moving turbulence (superleak); this material extends along part of the duct and completely occupies its internal cross-sectional area. The circulating duct includes a pumping device capable of maintaining a pressure difference across this body. The said body and at least part of the duct situated at the lower-pressure side of the body are thermally insulated, and the part of the duct in communication with the higher-pressure side of the body being in thermal contact with a cooler in which a temperature prevails below the point of He. The dimensions of the internal cross-sectional area of the duct and the pumping device are chosen so that in flowing through them, the medium exceeds its critical velocity with consequent turbulence. The body of material characterized in that normal He cannot flow through it, but superfluid He* can without the occurrence of turbulence, will hereinafter be referred to as a superleak.
The apparatus in accordance with the invention utilizes the fact that when in a U-shaped tube containing He at a temperature below the point, there is provided a superleak across which a temperature difference prevails, a driving force is exerted on the superfluid helium which causes it to flow through the superleak towards the high temperature. This flow of superfluid helium continues until there is produced in the limbs of the U-shaped tube a difference in level which produces a pressure difference across the superleak, which compensates for the driving force which acts on the superfluid helium owing to the temperature diiference. Conversely, the production of a pressure difference across the superleak will give rise to a temperature diiference across it. If, now, an artticle is to be cooled at this low temperature, it will be brought into contact with the helium at this area. During the cooling process, however, heat from the article will be continuously supplied to the medium and will have to be carried away by the helium, however, exhibits entropy and hence heat will be that its entropy is zero so that it cannot transfer heat.
ice
The apparatus according to the invention is based on the recognition that a continuous cooling process is obtained owing to the fact that turbulence will occur in the superfluid helium in the circulating duct, and that owing to the interaction of the turbulence in the superfluid helium on the normal helium, the latter will be carried along by the flow of superfluid helium. This entrained normal helium, however, exhibits entropy and hence heat will be carried along by this normal helium from the cold area to the cooled area at the higher temperature. This provides a surprisingly simple apparatus by means of which, starting from a temperature below the A point of the helium, cold may be produced at lower temperatures.
In a further advantageous embodiment of the apparatus in accordance with the invention, the thermally insulated part of the device is disposed in a vacuum chamber which is surrounded by a bath of liquid He at a temperature below the A point, the part of the duct protruding from the vacuum chamber being also surrounded by the liquid He. Thus, in this apparatus the heat which may be withdrawn from an article to be cooled at 0.7 K. on the cold side of a superleak is transported to the He bath.
In a further embodiment of the apparatus in accordance with the invention, the pumping device takes the form of a centrifugal pump disposed in the part of the duct protruding from the thermal insulation. The circulating duct need not be a closed duct of constant cross-section. The nonthermally insulated part, i.e. the part at the higher temperature, may include a container which is also filled with He*.
In a further advantageous embodiment the part of the duct situated in the path of the liquid He may be interrupted. Thus, the He bath ellectively forms part of the duct. This is possible since the duct contains the same medium as the surrounding bath.
The invention will now be described more fully with reference to the accompanying drawing, in which FIG- URES 1 and 2 show schematically and not to scale two embodiments of the apparatus in accordance with the invention.
The apparatus shown in FIGURE 1 includes a circulating duct 1, containing He A pumping device 2, a superleak 3 and a container 4 are disposed in the duct. The part of the duct constituted by the superleak 3, the container 4- and a pipe 5, is located in a vacuum chamber 6 which, through a pipe 7, is connected to a vacuum pump, not shown, to maintain the desired vacuum in the chamher 6. The part of the duct 1 protruding from the chamber 6 and accommodating the pump 2 is surrounded by liquid He which also surrounds the chamber 6 and is contained in a Dewar flask. By means of a vacuum pump, not shown, the vapour pressure above the liquid helium in the Dewar flask 8 is reduced to a value such that the temperature of the liquid helium in the flask 8 is lower than the temperature of the A point of helium. The temperature may, for example, be 13 K. The pump 2 is connected through a shaft 9 to a driving device, not shown. The apparatus operates as follows: On rotation of the pump 2 a higher pressure will be produced on the upper side of the superleak 3 at the area 10 and will drive the superfluid helium through the superleak. The superleak 3 may be in the form of pressed or sintered very finely divided substances, such as carborundum or iron oxide. The normal helium cannot pass through this superleak, preventing the convection of heat through it. Owing to the pressure difference across the superleak 3 a lower temperature will prevail in the container 4 than at the area 10. An article 11 to be cooled may be disposed in the container 4.
The part 5 of the duct is proportioned so that the superfluid helium exceeds its critical velocity therein with consequent turbulence. Owing to the interaction of the turbu- 3 lence of the superfluid helium, part of the normal helium will be carried along towards the pump. By this normal helium, heat will be carried away from the container 4 towards the pump. At an area 12 the circulating medium comes into heat-exchange with the helium bath so that it will again be brought to the temperature of this bath. Thus, an amount of heat will be transferred from the container 4, which is at a low temperature of, for example, 0.7 K., to the helium bath, which is at a temperature of, say, 1.3 K. This provides a cooling apparatus in which the superfluid helium when flowing through the superleak 3 to the container 4 transfers no heat, whereas the superfluid helium when flowing from the container 4 to the pump 2 through the capillary 5, in which turbulence occurs, is capable of entraining some normal helium so as to produce heat convection.
FIGURE 2 shows an apparatus which broadly corresponds to the apparatus shown in FIGURE 1. The difference is that the part of the duct 1 which is surrounded by the He bath is interrupted so that the capillary opens into the bath and the suction side of the pump 2 is connected to the bath. Thus, the bath efiFectively forms a buffer chamber for the duct. The operation of this apparatus is identical to that of the apparatus of FIGURE 1.
What is claimed is:
1. A method of transferring heat between low and high temperature levels, both levels being below the temperature of the A point of the He comprising the steps:
(a) flowing superfluid He through a superleak, thereby reducing the temperature of this He*;
(1)) flowing said reduced temperature He into a thermally insulated container housing an object to be cooled;
(c) absorbing heat from said object with some of said superfluid He which is thereby converted to normal He;
(d) flowing said superfluid He turbulently from the container through a duct dimensioned such that the superfluid He will flow turbulently;
(e) entraining said normal He with the turbulent flow of said superfluid He*.
2. A method as defined in claim 1 comprising the further steps of pumping said superfluid He through said superleak.
3. A method as defined in claim 2 comprising the further steps of flowing said superfluid He and normal He from said container to a pump, pumping said He to said superleak, and cooling said He to a temperature below the A point before it reaches the superleak.
4. A method as defined in claim 3 comprising the further steps of immersing said pump, container and duct in a quantity of superfluid He within a Dewar.
5. Apparatus for use with a source of superfluid He 4 for transferring heat between low and high temperature levels, both levels being below the temperature of the A point of the He*, comprising:
(a) a superleak formed of material permeable to the flow therethrough of superfluid He and impermeable to the flow of normal He'*;
(b) means for providing a pressure difference across the superleak, with resulting high and low pressure sides of the superleak and a temp-difference thereacross when superfluid He flows therethrough;
(c) means for cooling the fiuid entering the high-pressure side of the superleak to a temperature below the A point of He;
(d) a container for housing an object to be cooled and into which said superfluid He from the superleak is fiowable;
(e) a duct extending from said container to said source;
(f) means for thermally insulating the container and at least substantial parts of the superleak and the duct, and
(g) the duct being dimensioned such that superfluid He is fiowable therethrough from the container at a greater than critical velocity and to thereby flow turbulently and entrain the normal He into which heat from said object is absorbable.
6. Apparatus as defined in claim 5 wherein said means for providing a pressure difference is a pump.
7. Apparatus as defined in claim 5 further comprising a vacuum chamber housing for providing said thermal insulation.
8. Apparatus as defined in claim 5 wherein said duct discharges into said pump intake, thereby providing a closed circulatory system.
9. Apparatus as defined in claim 7 further comprising a Dewar containing liquid He at a temperature below its )1 point and in which said chamber and means for providing a pressure difference are immersed.
10. Apparatus as defined in claim 9 wherein said duct discharges into said liquid He in the Dewar, and the means providing a pressure difference is a pump which intakes liquid He from the Dewar.
References Cited UNITED STATES PATENTS 3,195,322 7/1965 London 62--5l4 3,364,687 1/1968 Kolm 62-467 3,376,712 4/1968 London 62-467 LLOYD L. KING, Primary Examiner US. Cl. X.R. 62-467 g 33; UNITED STAIES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 3 038 Dated October l 69 Inventore) FRANS ADRIANUS STAAS It is certified that error appears in the ab0-. -:identified patent and that said Letters Patent are hereby corrected as shown below:
Col. 1, line 70, after "helium" delete however exhibits entropy and hence heat will be" and insert Superfluid helium, however, has the property-- Signed and sealed this 1 th day of May 1 971 (SEAL) Attest:
EDWARD M.FLETCHER,JR. WILLIAM E. SCHUYLER, JR. Attesting Officer Commissioner of Patents
US722693A 1967-04-22 1968-04-19 Apparatus and method for transferring heat from a lower temperature level to a higher temperature level Expired - Lifetime US3472038A (en)

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DE (1) DE1751185A1 (en)
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3581512A (en) * 1968-06-05 1971-06-01 Philips Corp Liquid helium refrigeration apparatus and method
US3589138A (en) * 1968-06-05 1971-06-29 Philips Corp Device for transporting thermal energy from a lower to higher temperature level
US3835662A (en) * 1972-03-18 1974-09-17 Philips Corp Device for transporting heat from a lower to a higher temperature level
US3896630A (en) * 1972-03-17 1975-07-29 Philips Corp Method for starting a {hu 3{b He-{hu 4{b He dilution refrigerator
US4203299A (en) * 1977-07-16 1980-05-20 Messer Griesheim Gmbh Apparatus for metering small amounts of a low boiling liquefied gas
US4228662A (en) * 1978-02-17 1980-10-21 Deutsche Forschungs- und Versuchsanstalt fur Luftund Raumfahrt e.V. Cryogenic apparatus
US4283948A (en) * 1979-12-21 1981-08-18 Air Products And Chemicals, Inc. Cryogenic air sampler
EP0089391A1 (en) * 1982-03-23 1983-09-28 International Business Machines Corporation Method and dilution refrigerator for cooling at temperatures below 1K

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3195322A (en) * 1961-09-22 1965-07-20 Atomic Energy Authority Uk Refrigerator employing helium
US3364687A (en) * 1965-05-03 1968-01-23 Massachusetts Inst Technology Helium heat transfer system
US3376712A (en) * 1966-03-16 1968-04-09 Atomic Energy Authority Uk Refrigerators operating at very low temperatures

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3195322A (en) * 1961-09-22 1965-07-20 Atomic Energy Authority Uk Refrigerator employing helium
US3364687A (en) * 1965-05-03 1968-01-23 Massachusetts Inst Technology Helium heat transfer system
US3376712A (en) * 1966-03-16 1968-04-09 Atomic Energy Authority Uk Refrigerators operating at very low temperatures

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3581512A (en) * 1968-06-05 1971-06-01 Philips Corp Liquid helium refrigeration apparatus and method
US3589138A (en) * 1968-06-05 1971-06-29 Philips Corp Device for transporting thermal energy from a lower to higher temperature level
US3896630A (en) * 1972-03-17 1975-07-29 Philips Corp Method for starting a {hu 3{b He-{hu 4{b He dilution refrigerator
US3835662A (en) * 1972-03-18 1974-09-17 Philips Corp Device for transporting heat from a lower to a higher temperature level
US4203299A (en) * 1977-07-16 1980-05-20 Messer Griesheim Gmbh Apparatus for metering small amounts of a low boiling liquefied gas
US4228662A (en) * 1978-02-17 1980-10-21 Deutsche Forschungs- und Versuchsanstalt fur Luftund Raumfahrt e.V. Cryogenic apparatus
US4283948A (en) * 1979-12-21 1981-08-18 Air Products And Chemicals, Inc. Cryogenic air sampler
EP0089391A1 (en) * 1982-03-23 1983-09-28 International Business Machines Corporation Method and dilution refrigerator for cooling at temperatures below 1K

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CH482997A (en) 1969-12-15
FR1560167A (en) 1969-03-14
NL6705713A (en) 1968-10-23
GB1228029A (en) 1971-04-15
NO123965B (en) 1972-02-07
AT278065B (en) 1970-01-26
SE329639B (en) 1970-10-19
DE1751185A1 (en) 1971-06-03
BE714028A (en) 1968-10-22

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